Solutions Manual for Fluid Mechanics Seventh Edition in SI Units Chapter 4 Differential Relations for Fluid Flow PROPRIETARY AND CONFIDENTIAL PDF

Title Solutions Manual for Fluid Mechanics Seventh Edition in SI Units Chapter 4 Differential Relations for Fluid Flow PROPRIETARY AND CONFIDENTIAL
Author Alexis Han
Pages 69
File Size 9.9 MB
File Type PDF
Total Downloads 710
Total Views 801

Summary

Solutions Manual for Fluid Mechanics Seventh Edition in SI Units Frank M. White Chapter 4 Differential Relations for Fluid Flow PROPRIETARY AND CONFIDENTIAL This Manual is the proprietary property of The McGraw-Hill Companies, Inc. (“McGraw-Hill”) and protected by copyright and other state and feder...


Description

Solutions Manual for

Fluid Mechanics Seventh Edition in SI Units

Frank M. White Chapter 4 Differential Relations for Fluid Flow

PROPRIETARY AND CONFIDENTIAL This Manual is the proprietary property of The McGraw-Hill Companies, Inc. (“McGraw-Hill”) and protected by copyright and other state and federal laws. By opening and using this Manual the user agrees to the following restrictions, and if the recipient does not agree to these restrictions, the Manual should be promptly returned unopened to McGraw-Hill: This Manual is being provided only to authorized professors and instructors for use in preparing for the classes using the affiliated textbook. No other use or distribution of this Manual is permitted. This Manual may not be sold and may not be distributed to or used by any student or other third party. No part of this Manual may be reproduced, displayed or distributed in any form or by any means, electronic or otherwise, without the prior written permission of the McGraw-Hill. © 2011 by The McGraw-Hill Companies, Inc. Limited distribution only to teachers and educators for course preparation. If you are a student using this Manual, you are using it without permission.

P4.1 An idealized velocity field is given by the formula

Is this flow field steady or unsteady? Is it two- or three-dimensional? At the point (x, y, z) = (–1, +1, 0), compute (a) the acceleration vector and (b) any unit vector normal to the acceleration. Solution: (a) The flow is unsteady because time t appears explicitly in the components. (b) The flow is three-dimensional because all three velocity components are nonzero. (c) Evaluate, by laborious differentiation, the acceleration vector at (x, y, z) = (−1, +1, 0). du ∂ u ∂u ∂u ∂u = +u +v +w = 4x + 4tx(4t) − 2t 2 y(0) + 4xz(0) = 4x +16t 2 x ∂x ∂y ∂z dt ∂ t ∂v ∂v ∂v dv ∂ v = + u + v + w = −4ty + 4tx(0) − 2t 2 y(−2t 2 ) + 4xz(0) = −4ty + 4t 4 y dt ∂ t ∂x ∂y ∂z dw ∂ w ∂w ∂w ∂w = +u +v +w = 0 + 4tx(4z) − 2t 2 y(0) + 4xz(4x) = 16txz +16x 2 z ∂t ∂x ∂y ∂z dt or:

dV = (4x +16t 2 x)i + (−4ty + 4t 4 y)j + (16txz +16x 2 z)k dt

at (x, y, z) = (−1, +1, 0), we obtain (d) At (–1, +1, 0) there are many unit vectors normal to dV/dt. One obvious one is k. Ans.

P4.2 A three-dimensional flow field has the velocity given by V = 4x 2 i + 3xyj + 5t(x + y)zk

Find the local and total accelerations in terms of x, y, z, and t. Solution

 Velocity V = (4x 2 , 3xy, 5t(x + y)z)  ∂V Local acceleration = (0, 0, 5(x + y)z) ∂t Convective acceleration

ax = u

∂u ∂u ∂u +v +w ∂x ∂y ∂z

= (4x 2 )(8x) + (3xy)(0) + 5t(x + y)z(0) = 32x 3

2

ay = u

∂v ∂u ∂u +v +w ∂x ∂y ∂z

= (4x 2 )(3y) + (3xy)(3x) + 5t(x + y)z(0) = 12x 2 y + 9x 2 y = 21x 2 y ∂w ∂w ∂w +v +w az = u ∂x ∂y ∂z = (4x 2 )(5tz) + (3xy)(5tz) + 5t(x + y)z(5t)(x + y) = 20tx 2 z +15txyz + 25t 2 (x + y)2 z

Total acceleration = Local accel + convective accel  ∂v = (32x 3 , 21x 2 y, 20tx 2 z + 15txyz + 25t 2 (x + y)2 z + 5(x + y)z) ∂t

P4.3 Flow through the converging nozzle in Fig. P4.3 can be approximated by the onedimensional velocity distribution

(a) Find a general expression for the fluid acceleration in the nozzle. (b) For the specific case Vo = 3 m/s and L = 15 cm, compute the acceleration, in g’s, at the entrance and at the exit.

Fig. P4.3

Solution: Here we have only the single ‘one-dimensional’ convective acceleration:

For L = 0.15 m and Vo = 3 m/s,

du 2(3)2  2x  =  = 120(1+13.3x), with x in m 1+ dt 0.15  0.15 

At x = 0, du/dt = 120 m/s2 (12 g’s); at x = L = 0.15 m, du/dt = 360 m/s2 (37 g’s). Ans. (b)

3



P4.4 A two-dimensional velocity field is given by V = (x2 – y2 + x)i – (2xy + y)j in arbitrary units. At (x, y) = (1, 2), compute (a) the accelerations ax and ay, (b) the velocity component in the direction θ = 40°, (c) the direction of maximum velocity, and (d) the direction of maximum acceleration. Solution: (a) Do each component of acceleration:

du ∂u ∂u = u + v = (x 2 − y 2 + x)(2x +1) + (−2xy − y)(−2y) = a x ∂x ∂y dt dv ∂v ∂v = u + v = (x 2 − y 2 + x)( −2y) + (−2xy − y)(−2x −1) = a y dt ∂x ∂y At (x, y) = (1, 2), we obtain ax = 18i and ay = 26j Ans. (a) (b) At (x, y) = (1, 2), V = –2i – 6j. A unit vector along a 40° line would be n = cos40°i + sin40°j. Then the velocity component along a 40° line is

V40° = V⋅n40° = (−2i − 6 j) ⋅ (cos 40°i + sin 40°j) ≈ 5.39 units

Ans. (b)

(c) The maximum acceleration is amax = [182 + 262]1/2 = 31.6 units at ∠55.3° Ans. (c, d)

P4.5

A simple flow model for a two-dimensional converging nozzle is the distribution x u = U o (1+ ) L

v = −U o

y L

w=0

(a) Sketch a few streamlines in the region 0...


Similar Free PDFs